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EP0362705A2 - Olefinpolymerisationskatalysator - Google Patents

Olefinpolymerisationskatalysator Download PDF

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Publication number
EP0362705A2
EP0362705A2 EP89118027A EP89118027A EP0362705A2 EP 0362705 A2 EP0362705 A2 EP 0362705A2 EP 89118027 A EP89118027 A EP 89118027A EP 89118027 A EP89118027 A EP 89118027A EP 0362705 A2 EP0362705 A2 EP 0362705A2
Authority
EP
European Patent Office
Prior art keywords
dimethoxypropane
isopropyl
catalyst
compound
solid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP89118027A
Other languages
English (en)
French (fr)
Other versions
EP0362705A3 (de
EP0362705B1 (de
Inventor
Pier Camillo Dr. Barbe'
Luciano Dr. Noristi
Raimondo Scordamaglia
Luisa Barino
Enrico Albizzati
Umberto Dr. Giannini
Giampiero Dr. Morini
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Basell North America Inc
Original Assignee
Himont Inc
Montell North America Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Himont Inc, Montell North America Inc filed Critical Himont Inc
Publication of EP0362705A2 publication Critical patent/EP0362705A2/de
Publication of EP0362705A3 publication Critical patent/EP0362705A3/de
Application granted granted Critical
Publication of EP0362705B1 publication Critical patent/EP0362705B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/646—Catalysts comprising at least two different metals, in metallic form or as compounds thereof, in addition to the component covered by group C08F4/64
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/65—Pretreating the metal or compound covered by group C08F4/64 before the final contacting with the metal or compound covered by group C08F4/44
    • C08F4/652—Pretreating with metals or metal-containing compounds
    • C08F4/658—Pretreating with metals or metal-containing compounds with metals or metal-containing compounds, not provided for in a single group of groups C08F4/653 - C08F4/657

Definitions

  • Catalysts containing titanium compounds supported on magnesium halides in active form are well known in the art.
  • catalysts described in European patent No. 0045977 comprise a solid catalyst component containing magnesium dihalide in active form on which is supported a titanium halide (TiCl4) and an electron-­donor compound selected from specific classes of carboxylic acid esters, of which the phthalates are typical preferred relevant examples.
  • TiCl4 titanium halide
  • an electron-­donor compound selected from specific classes of carboxylic acid esters, of which the phthalates are typical preferred relevant examples.
  • co-catalysts a system formed of an Al-­alkyl compound and a silicon compound having at least one Si-OR bond, where R is a hydrocarbon radical, is used.
  • the electron donors mentioned comprise silicon compounds with Si-OR bonds, 2,2,6,6,-tetramethylpiperidine, 2,2,5,5-tetra­methylpyrrolidine, Al-diethyl-2,2,6,6-tetramethylpiperidine and Al-dichloromonophenoxy.
  • the electron donors used in the catalysts of the invention are selected from ethers containing two or more ether groups and capable of complexing anhydrous magnesium dichloride having a specific degree of activation for less than 60 mmoles per 100 g of MgCl2.
  • Ethers having the above mentioned characteristics are 1,3-diethers of the formula: in which R, R I , R II , R III , R IV and R V are the same or different and are H, linear or branched alkyl radicals, or cycloalkyl, aryl, alkylaryl or arylalkyl radicals with 1-18 carbon atoms, provided R and R′ and not both are hydrogen; R VI and R VII have the same meaning of R and R I except for hydrogen; provided that when R I to R V are hydrogen and R VI and R VII are methyl, R is not methyl; and one or more R to R VII can be linked to form a cyclic structure.
  • R is other than methyl.
  • ethers are: 2-(2-ethylhexyl)-1,3-dimethoxypropane, 2-isopropyl-1,3-dime­thoxypropane, 2-methyl-1,3-dimethoxypropane, 2-butyl-1,3-­dimethoxypropane, 2-sec-butyl-1,3-dimethoxypropane, 2-cyclo­hexyl-1,3-dimethoxypropane, 2-phenyl-1,3-dimethoxypropane, 2-­tert-butyl-1,3-dimethoxypropane, 2-cumil-1,3-diethoxypropane, 2-(2-phenyl ethyl)- 1,3 dimethoxypropane, 2-(2-cyclohexyl­ethyl)-1,3-dimethoxypropane, 2-(2-ethyl)- 1,3 dimethoxypropane, 2-(2-cyclohexyl
  • Suitable ethers are: 2,3-diphenyl-1,4-diethoxybutane, 2,3-dicyclohexyl-1,4-dietho­xybutane, 2,3-dibenzyl-1,4-diethoxybutane, 2,3-dibenzyl-1,4-­dimethoxybutane, 2,3-dicyclohexyl-1,4-dimethoxybutane, 2,3-diisopropyl-1,4-dimethoxybutane, 2,3-diisopropyl-1,4-­diethoxybutane, 2,2-bis-(p-methylphenyl)-1,4-dimethoxybutane, 2,3-bis-(p-chlorophenyl)-1,4-dimethoxybutane, 2,3-bis-(p-­fluorophenyl)-1,4-dimethoxybutane, 2,4-diphenyl-1,5-dimetho­ xybut
  • Preferred ethers are those having the general formula herein above and particularly those in which R VI and R VII are methyl and R and R I are the same or different and are isopropyl, isobutyl, t-butyl, cyclohexyl, isopentyl, ethylcyclohexyl, pentyl, cyclopentyl, heptyl, 1,5-dimethylhexyl, 3,7-dimethyloctyl, phenyl, cyclohexylmethyl and propyl.
  • the test of ether complexation of MgCl2 is carried out as follows. Into a 100 ml glass flask with a fixed blade glass stirrer under a nitrogen atmosphere 70 ml anhydrous n-­heptane, 12 mmols anhydrous MgCl2, activated as hereinafter described, and 2 mmols ethers was introduced and heated at 60 o for 4 hours with a stirring velocity of 400 rpm. The reaction mixture was filtered and washed at room temperature with 100 ml portions of n-heptane and then dried with a mechanic pump.
  • the complexation tests results are reported in Table I.
  • the magnesium dichloride used in the complexation test with ether was prepared as follows: in a vibratory mill jar (Siebtechnik Vibratom), having a 1 liter capacity and loaded with 1,8 Kg of steel spheres with 16 mm diameter, was introduced under nitrogen atmosphere 50 g anhydrous MgCl2 and 6,8 ml 1,2-dichloroethane (DCE).
  • Catalyst components usable with the electron donors of this invention are described in U.S. patent No. 4,522,930 the description of which is incorporated herein by reference.
  • the solid catalyst components described in the U.S. patent No. 4,522,930 comprise a titanium component with at least a Ti-halogen bond and an electron donor-­compound which is extractable with Al-triethyl under standard conditions of extraction for at least 70% by mol from the solid. After extraction, the solid has a surface area (B.E.T.) of at least 20 m2/g and in general comprised between 100 and 300 m2/g.
  • the electron-donor compounds suitable to prepare the catalyst components described in the U.S. patent include ethers, ketones, lactones, electron donors compounds with N, P and/or S atoms and specific classes of esters.
  • the esters described in the European patent 45,977 are also suitable.
  • esters of phtalic acid such as diisobutyl, dioctyl, diphenyl and benzyl-butylphtha­late
  • esters of malonic acid such as diisobutyl and diethylmalonate
  • alkyls and arylpivalates alkyl, cycloalkyl and arylmaleates
  • alkyl and aryl carbonates such as diisobutyl, ethyl-phenyl and diphenylcarbonate
  • succinic acid esters mono and diethyl succinate are the preferred donors.
  • the preparation of the solid catalyst components is carried out according to several methods.
  • the magnesium dihalide in an anhydrous state containing less than 1% water, the titanium compound and the electron-donor compound are milled together under conditions in which activation of the magnesium dihalide occurs.
  • the milled product is then treated one or more times with an excess of TiCl4 at a temperature between 80 and 135 o C, and then washed repeatedly with a hydrocarbon solvent such as hexane, until there are no chlorine ions in the water.
  • anhydrous magnesium dichloride is preactivated according to well known methods and then treated with an excess TiCl4 containing in solution an electron donor compound at a temperature of about 80 o to 135 o C.
  • the treatment with TiCl4 is repeated and the solid is washed with hexane to eliminate any non-reacted TiCl4.
  • an adduct MgCl2.nROH (especially in the form of spherical particles) in which n is 1 to 3 and ROH is ethanol, butanol, isobutanol, is treated with an excess TiCl4 containing an electron-donor compound in solution at a temperature of about 80 and 120 o C. After reaction, the solid is again treated with TiCl4, then separated and washed with hydrocarbon until the chlorine ions are removed.
  • magnesium alcoholates or chloroalcoholates are reacted with an excess of TiCl4 containing in solution an electron-donor compound, operating also under the reaction conditions described above.
  • complexes of magnesium halides with titanium alcoholates are reacted in hydrocarbon solution with an excess of TiCl4 containing in solution an electron-donor compound; the solid product is separated and then further reacted with an excess of TiCl4 at 80 o -120 o C. The solids were then separated and washed with hexane.
  • the complex between MgCl2 and the titanium alcoholate is reacted in an hydrocarbon solution with hydropolyxylosane.
  • the solid product is separated and reacted at 50 o C with silicon tetrachloride containing in solution an electron-donor compound.
  • the solid is then reacted with excess TiCl4 at 80 o -­100 o C.
  • porous resins which can be used in the present invention and their impregnation method are described in U.S. patent application Serial No. 07/359,234.
  • Reaction with TiCl4 is carried out at 80-100 o C; after separating the TiCl4 excess, the reaction is repeated and the solid is then washed with hydrocarbon.
  • the molar ration between MgCl2 and the electron-donor compound used in the above described reactions is between 4:1 and 12:1.
  • the amount of electron-donor compound which remains fixed on the magnesium dihalide is between 5 and 20 mole %.
  • the molar ratio between the electron-donor compound and magnesium is higher and in general comprised between 0.3 and 0.8.
  • the ratio Mg/Ti is usually between 30:1 and 4:1.
  • the ratio is lower and is generally between 3:1 and 2:1.
  • Suitable titanium compounds used for the preparation of the solid catalyst components are the halides and the halo­alcoholates. Titanium tetrachloride is the preferred compound. Satisfactory results are also obtained with Ti-­trihalides in particular TiCl3-HR, TiCl3-ARA, and with haloalcoholates like TiCl3 OR in which R is a phenyl radical.
  • Ti-­trihalides in particular TiCl3-HR, TiCl3-ARA, and with haloalcoholates like TiCl3 OR in which R is a phenyl radical.
  • R is a phenyl radical.
  • the above mentioned reactions lead to the formation of magnesium halides in active form. Besides these reactions, other reactions are well known in literature which form magnesium halides in active form starting from magnesiums compounds different from the halides.
  • the active form of magnesium dihalides in the solid catalyst components is evidenced in X-rays spectrum of the catalyst component in which the most intense reflection line appearing in the spectrum of non-activated magnesium dihalide having a surface area less than 3 m2/gr, is absent and substituted by a halo with the maximum of intensity shifted with respect to the position of the most intense reflection line, or from the fact that the most intense reflection line shows a half peak breadth of at least 30% greater than the breadth of the most intense reflection line appearing in the spectrum of non-activated Mg dihalide.
  • the most active forms are those in which the halo appears in the X-rays spectrum of the solid catalyst component.
  • the highly preferred magnesium halides is magnesium dichloride.
  • the X-ray spectrum of the catalyst component shows a halo in place of the most intense diffraction line that in the spectrum of non-activated magnesium dichloride which appears at a distance of 2.56 ⁇ .
  • the Al-­alkyl compounds are selected from the Al-trialkyls such as Al-triethyl, Al-triisobutyl, Al-tri-n-butyl and linear or cyclic Al-alkyl compounds containing two or more atoms of Al linked each other through an oxygen or a nitrogen atom or through SO4 and SO3 groups. Examples of these compounds are: in which n is a number from 1 to 20.
  • AlR2OR I compounds in which R I is an aryl radical substituted in one or both or ortho positions and R is an alkyl radical with 1-6 carbon atoms
  • AlR2H compounds in which R has the meaning as above indicated are also suitable.
  • the Al-alkyl compound is an amount such that the ratio of Al/Ti is between 1 and 1000.
  • the trialkyl compounds may be used in mixture with Al-alkyl halides such as AlEt2Cl.
  • the catalysts of the invention include the product of the reaction between the following components:
  • Olefin polymerization is carried out according to known methods in liquid phase using the liquid monomer or a solution of liquid monomer or monomers in an aliphatic or aromatic hydrocarbon solvent, in gas phase or in a combination of in liquid phase and gas phase processes.
  • the temperature of (co)polymerization is generally from 0 o to 150 o C; in particular between 60 o and 100 o C.
  • the polymerizations are carried out at atmospheric or higher pressure.
  • the catalysts can be precontacted with small quantities of olefin monomer (prepolymerization). Prepolymerization improves the catalysts performance as well as polymer morphology.
  • Prepolymerization is carried out by maintaining the catalyst in suspension in a hydrocarbon solvent (hexane, heptane, etc) at a temperature range from room temperature to 60 o C for a time sufficient to produce a quantity of polymer from 0.5 to 3 times the weight of the solid catalyst component.
  • Prepolymerization can also be carried out in liquid propylene under the same conditions of temperature as above to produce up to 1000 g polymer per g of catalyst component.
  • the molar ratio between the Al-alkyl compound and the ether donor is in general from 5:1 to 100:1.
  • the autoclave was closed. After having set the pressure at 1 atm, 0.2 atm hydrogen was introduced and the contents heated at 70 o C while feeding propylene up to the total pressure of 7 atm.
  • the polymerization was carried out for 2 hours. During that period monomer feeding was continued. The polymer was isolated by filtration at the end of the reaction period, and vacuum dried. The remaining portion of polymer in the filtrate was precipitated with methanol, vacuum dried and considered in determining the total residue extractable with n-heptane.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
EP89118027A 1988-09-30 1989-09-29 Olefinpolymerisationskatalysator Expired - Lifetime EP0362705B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT2215188 1988-09-30
IT8822151A IT1227259B (it) 1988-09-30 1988-09-30 Catalizzatori per la polimerizzazione di olefine.

Publications (3)

Publication Number Publication Date
EP0362705A2 true EP0362705A2 (de) 1990-04-11
EP0362705A3 EP0362705A3 (de) 1991-05-02
EP0362705B1 EP0362705B1 (de) 1995-01-11

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EP89118027A Expired - Lifetime EP0362705B1 (de) 1988-09-30 1989-09-29 Olefinpolymerisationskatalysator

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US (1) US4978648A (de)
EP (1) EP0362705B1 (de)
JP (1) JP2774160B2 (de)
KR (1) KR0140221B1 (de)
CN (1) CN1015806B (de)
AR (1) AR247576A1 (de)
AT (1) ATE116997T1 (de)
AU (1) AU610019B2 (de)
BR (1) BR8904953A (de)
CA (1) CA1337411C (de)
CZ (1) CZ278377B6 (de)
DE (1) DE68920528T2 (de)
ES (1) ES2065963T3 (de)
FI (1) FI95277C (de)
HU (1) HU206507B (de)
IL (1) IL91741A (de)
IT (1) IT1227259B (de)
MX (1) MX17762A (de)
MY (1) MY110248A (de)
NO (1) NO174627C (de)
PH (1) PH27289A (de)
PT (1) PT91866B (de)
RU (1) RU2081883C1 (de)
YU (1) YU187989A (de)
ZA (1) ZA897444B (de)

Cited By (35)

* Cited by examiner, † Cited by third party
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EP0452156A3 (en) * 1990-04-13 1992-05-06 Mitsui Petrochemical Industries, Ltd. Solid titanium catalyst component for olefin polymerization, olefin polymerization catalyst, prepolymerized polyolefin-containing catalyst and method of olefin polymerization
EP0451645A3 (en) * 1990-03-30 1992-09-02 Himont Inc Components and catalysts for the polymerization of olefins
EP0622380A1 (de) * 1993-04-29 1994-11-02 Montell North America Inc. Kristalline Propylenpolymere, die eine hohe Schmelzflussrate und eine enge Molekulargewichtsverteilung aufweisen
US5529850A (en) * 1994-07-05 1996-06-25 Montell North America Inc. Fibers produced from crystalline propylene polymers having high melt flow rate values and a narrow molecular weight distribution
EP0719798A1 (de) * 1994-12-29 1996-07-03 Montell Technology Company bv Verfahren zur (Co)Polmerisation von Ethylen
EP0719800A1 (de) * 1994-12-29 1996-07-03 Montell Technology Company bv Katalysatore für die (Co)Polymerisation von Ethylen
EP0719799A1 (de) * 1994-12-29 1996-07-03 Montell Technology Company bv Katalysatore für die (Co)Polymerisation von Ethylen
EP0728769A1 (de) * 1995-02-21 1996-08-28 Montell North America Inc. Komponente und Katalysatore für die Olefinpolymerisation
US5648422A (en) * 1994-10-05 1997-07-15 Montell Technology Company Bv Process for the (co)polymerization of olefins
WO1997031954A1 (en) * 1996-02-27 1997-09-04 Montell North America Inc. Process for the preparation of random propylene copolymers and products obtained therefrom
US5726262A (en) * 1990-04-13 1998-03-10 Mitsui Petrochemical Industries, Ltd. Solid titanium catalyst component for olefin polymerization, olefin polymerization catalyst, prepolymerized polyolefin-containing catalyst and method of olefin polymerization
US5869418A (en) * 1994-05-31 1999-02-09 Borealis Holding A/S Stereospecific catalyst system for polymerization of olefins
US6100333A (en) * 1995-05-11 2000-08-08 Montell Technology Company B.V. Dynamically vulcanizable polyolefin compositions
WO2000058371A1 (en) * 1999-03-30 2000-10-05 Eastman Chemical Company Process for producing polyolefins
US6262195B1 (en) 1998-03-09 2001-07-17 Montell Technology Company Bv Multi-stage process for the polymerization of olefins
US6423800B1 (en) 1999-05-26 2002-07-23 Fina Technology, Inc. Pelletized polyolefin having ultra-high melt flow and its articles of manufacture
WO2002062855A1 (en) * 2001-02-08 2002-08-15 Ube Industries, Ltd. CATALYST FOR α-OLEFIN POLYMERIZATION AND METHOD OF POLYMERIZATION WITH THIS CATALYST
US6436864B1 (en) 1999-10-06 2002-08-20 Sri International Unsaturated nitrogenous compounds as electron donors for use with ziegler-natta catalysts
WO2002100904A1 (en) * 2001-06-13 2002-12-19 Basell Poliolefine Italia S.P.A Components and catalysts for the (co)polymerization of olefins
US6541582B1 (en) * 1999-03-15 2003-04-01 Basell Poliolefine Italia S.P.A. Components and catalysts for the polymerization of olefins
US6818583B1 (en) 1999-04-15 2004-11-16 Basell Poliolefine Italia S.P.A. Components and catalysts for the polymerization of olefins
US6992153B1 (en) 1999-03-09 2006-01-31 Basell Polyolefine Gmbh Multi-stage process for the (CO) polymerization of olefins
US7365137B2 (en) 2001-07-17 2008-04-29 Basell Polyolefine Gmbh Multistep process for the (co) polymerization of olefins
WO2008061662A1 (en) * 2006-11-21 2008-05-29 Basell Poliolefine Italia S.R.L. Catalyst component for the polymerization of olefins
EP1816146A4 (de) * 2004-11-17 2009-02-25 Mitsui Chemicals Inc Feste titankatalysatorkomponente, katalysator für die olefinpolymerisation und verfahren zur herstellung von oelfinpolymer
US7572859B2 (en) 2002-06-26 2009-08-11 Basell Polyolefine Italia S.R.L. Impact-resistant polyolefin compositions
US7700690B2 (en) 2002-06-26 2010-04-20 Basell Poliolefine Italia S.R.L. Impact-resistant polyolefin compositions
WO2010076701A1 (en) 2008-12-30 2010-07-08 Basell Poliolefine Italia S.R.L. Process for producing high melt strength polypropylene
US8039540B2 (en) 2004-06-08 2011-10-18 Basell Poliolefine Italia S.R.L. Polyolefin composition having a high balance of stiffness, impact strength and elongation at break and low thermal shrinkage
US8058350B2 (en) 2003-11-06 2011-11-15 Basell Poliolefine Italia, s.r.l. Polypropylene composition
US8378028B2 (en) 2008-02-29 2013-02-19 Basell Poliolefine Italia, s.r.l. Polyolefin compositions
US8394734B2 (en) 2011-04-27 2013-03-12 Samsung Total Petrochemicals Co., Ltd. Solid catalyst for propylene polymerization and a method for preparation of polypropylene using the same
EP2816062A1 (de) 2013-06-18 2014-12-24 Basell Poliolefine Italia S.r.l. Vorpolymerisierte Katalysatorkomponenten zur Polymerisierung von Olefinen
EP3653631A1 (de) * 2012-09-24 2020-05-20 INDIAN OIL CORPORATION Ltd. Prozesse für die herstellung von olefin polimerisationskatalysatoren die auf der behandlung von festen organomagnesiumverbindungen mit titan einheiten basieren
WO2022214328A1 (en) 2021-04-06 2022-10-13 Basell Poliolefine Italia S.R.L. Pre-polymerized catalyst components for the polymerization of olefins

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IT1227258B (it) * 1988-09-30 1991-03-28 Himont Inc Componenti e catalizzatori per la polimerizzazione di olefine
US5221651A (en) * 1989-04-28 1993-06-22 Himont Incorporated Component and catalysts for the polymerization of olefins
IT1256648B (it) * 1992-12-11 1995-12-12 Montecatini Tecnologie Srl Componenti e catalizzatori per la polimerizzazione delle olefine
IT1264679B1 (it) * 1993-07-07 1996-10-04 Spherilene Srl Catalizzatori per la (co)polimerizzazione di etilene
TW354792B (en) 1993-08-13 1999-03-21 Mitsui Petrochemical Ind Olefin polymerization catalyst and process for preparing polypropylene and propylene block copolymer
EP0668296B1 (de) * 1994-02-18 1998-05-06 Mitsui Petrochemical Industries, Ltd. Ethylenpolymer und Verfahren zur Herstellung desselben
US7049377B1 (en) * 1995-02-21 2006-05-23 Basell Poliolefine Italia S.R.L. 1,3-diethers and components and catalysts for the polymerization of olefins, containing said diethers
US5747407A (en) * 1996-08-29 1998-05-05 Phillips Petroleum Company Method of making a Ziegler-Natta olefin polymerization catalyst
KR100334167B1 (ko) * 1997-05-08 2002-11-22 삼성종합화학주식회사 알파-올레핀중합방법
GB2325004B (en) * 1997-05-09 1999-09-01 Samsung General Chemicals Co A catalyst for polymerization and copolymerization of olefins
KR100240519B1 (ko) * 1997-09-11 2000-01-15 유현식 새로운 올레핀 중합용 킬레이트 촉매 및 이를 이용한 올레핀중합 방법
SG73622A1 (en) * 1998-03-11 2000-06-20 Sumitomo Chemical Co Solid catalyst component and catalyst for olefin polymerization and process for producing olefin polymer
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KR0140221B1 (ko) 1998-07-01
PT91866A (pt) 1990-03-30
US4978648A (en) 1990-12-18
CZ278377B6 (en) 1993-12-15
CN1015806B (zh) 1992-03-11
CN1042157A (zh) 1990-05-16
CZ554489A3 (en) 1993-04-14
MX17762A (es) 1993-12-01
YU187989A (en) 1990-12-31
IT8822151A0 (it) 1988-09-30
FI894627L (fi) 1990-03-31
ZA897444B (en) 1990-07-25
NO174627B (no) 1994-02-28
IT1227259B (it) 1991-03-28
JPH02255810A (ja) 1990-10-16
MY110248A (en) 1998-03-31
AU4252689A (en) 1990-04-05
PT91866B (pt) 1995-05-31
ATE116997T1 (de) 1995-01-15
IL91741A0 (en) 1990-06-10
NO174627C (no) 1994-06-08
DE68920528T2 (de) 1995-07-13
DE68920528D1 (de) 1995-02-23
ES2065963T3 (es) 1995-03-01
BR8904953A (pt) 1990-05-08
HU206507B (en) 1992-11-30
HUT52794A (en) 1990-08-28
KR900004773A (ko) 1990-04-13
FI95277C (fi) 1996-01-10
AU610019B2 (en) 1991-05-09
EP0362705A3 (de) 1991-05-02
CA1337411C (en) 1995-10-24
JP2774160B2 (ja) 1998-07-09
FI894627A0 (fi) 1989-09-29
NO893898D0 (no) 1989-09-29
IL91741A (en) 1993-06-10
NO893898L (no) 1990-04-02
FI95277B (fi) 1995-09-29
AR247576A1 (es) 1995-01-31
PH27289A (en) 1993-05-04
EP0362705B1 (de) 1995-01-11
RU2081883C1 (ru) 1997-06-20

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